reliance conference presentation

7/24/2019 Reliance Conference Presentation

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Disclaimer

Any statement, opinion, prediction, comment, or observation made in this

presentation/publication are those of the presenter/author only and in no conditionshould be construed necessarily representing the policy and intent of Reliance

Industries Ltd. (RIL).

The information presented herein are of the presenter/authors own and in no way RIL

attracts any liability for any inconsistency or irregularity in terms of the accuracy

completeness, veracity, or truth of the content of the presentation/publication. In

addition, RIL shall not be liable for any copyright infringement and misrepresentation for

the presented content as the content is presumed in good faith to be a creation of

presenters/authors own mind.

The scope of this presentation/publication is strictly for knowledge sharing purposes and

not necessarily to provide any advice or recommendation to the audience/readers. Any

endorsement, recommendation, suggestion, or advice made by the presenter/authorshall be in his personal capacity and not in professional capacity as an employee of RIL.

Any person acting on such endorsement, recommendation, suggestion, or advice will

himself/herself be responsible for any injury/damage.

Reliance Industries Ltd.


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Index

Fundamentals

Crude flexibility

Petrochemical Integration

Conclusion


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Refinery competitiveness: Fundamentals

2 mantras for refinery competitiveness

Minimize feed costs

Low crude cost crude flexibility : Sourcing

: Processing

: Quality

Low opex

Maximize product revenues

High value product petrochemical integration

Distillates = Jet + diesel + gasoline


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Crude flexibility: Sourcing

Max crude sourcing flexibility

Quantity

Process 1358 kb/d of crude (FY15)

Source crude globally

Quality

Refine 144 crude grades from 1999 (16 years)

Virtually any crude grade can be refined

No constraints on crude properties

Refine 13 new crude grades (FY15)

Refine new crude grades Jamnagar is the destination of choice for novel crude

Eg. Basra heavy (FY15)

Process any distressed crude cargo


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Crude flexibility: Processing

Max crude processing flexibility

Dilution - 1358 kb/d of crude, large pool for dilution

- VLCC = 60 kb/d or 4.4% of crude feed

- Suez Max = 45 kb/d or 3.3% of crude feed

- Afra Max = 30 kb/d or 2.2% of crude feed

- Refine any crude grade by dilution principle

Sequencing & Scheduling - Sequence optimal arrivals of crude grades

- Crude scheduling to enable optimal blending

- GeCOS system (Shell)

Blending - Process crude grades with wide range of qualities

- Blend to narrow crude feed window

- Minimal variation seen by refinery CDU/VDU

- TIS / OMS system (Schneider)


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Crude flexibility: Quality

Max crude quality flexibility

API = From 130API to 560API

- Peregrino (Brazil) = 13.4API

- Ras Gas condensate = 560API

Sour = From 0 to 6.7 wt%

- Coban (Guatemala), S = 6.7 %

Acidic = From 0 to 5.3 TAN

- Olende (Gabon), TAN = 5.3 mg KOH

Metals = From 0 to 450 ppm Ni + V

- Napo (Equador), Ni + V = 450 ppm

Synthetic crudes = From bitumen upgraders

- Hamaca (Venezuela)

- Cold Lake (Canada)


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Petrochemical integration: Value Addition

Max value addition to petrochemicals

Product $/t % of Crude

Petrochemicals:

PX 825-845 198

Propylene 760-780 183

Ethylene 740-760 178

Distillates:

Jet 575-585 138

Diesel 555-565 133

Gasoline 545-555 131

Others

Naphtha 470 112

LPG 460 110

Fuel gas 440 104

Crude 420 Base

Basis = Crude @ $60/bbl


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Petrochemicals integration: Jamnagar refinery

Maximize margins

Propylene : 2 mmt/yr propylene @ 3% of crude

: 2 FCC @ 420 kb/d

: 100% captive consumption to PP

: Advantage feed = Hydrotreated VGO to FCC

Aromatics : 5.45 mmt/yr Aromatics @ 8.1% of crude

: 2 Platformer @ 190 kb/d

: 4.2 mmt/yr PX

: Advantage feed = Reformate

ROG Cracker : 1.8 mmt/yr ethylene derivatives

: 2.7% of crude

: Advantage feed = Refinery off gas (ROG)

: Gasification enabled = Swap SNG for Cracker feed


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Petrochemicals: Propylene

Value addition to propylene + PP

FCC : 2 units, combined capacity = 420 kb/d

: Worlds largest FCC (UOP)

: Moderate severity, >10% C3= yields

: 2 mmt/yr of propylene

PRU : 3 units

: C3 splitter design with heat pump (UOP)

PP : 6 PP lines, 4 275 kt/yr + 2 450 kt/yr

: Combined capacity = 2 mmt/yr PP

: Gas phase bulk polymer (Dow)

: Worlds largest PP complex


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Petrochemicals: Aromatics

Worlds largest PX complex

Aromatics DTA SEZ/PX-4 Total

CCR reformer, kb/d 90 100 190

PX, mmt/yr 1.9 2.3 4.2

OX, mmt/yr 0.3 0 0.3

Benzene, mmt/yr 0.4 0.55 0.95

Total Aromatics, mmt/yr 2.6 2.85 5.45

Process Selective adsorption Crystallization

Parex / Isom trains 3 / 3 0 / 1

Crystallizers / Centrifuges 0 3

Trans alkylation 2 1Extractive distillation 1 1

Licensor UOP BP / Lummus

Status Operating Construction


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Petrochemicals: Integrated Aromatics

Global #2 in polyester

Crude to naphtha to PX @ Jamnagar refinery

PX to PTA to PET @ Dahej

PX to PTAto Polyester @ Silvassa + Hazira

PTA to Polyester @ Silvassa Integrated polyester value chain


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Petrochemicals: ROG Cracker

Worlds largest ROG Cracker

Feed : Extract C2

+ C2

= from refinery offgas (ROG)

: Rich feed = 27% C2= in feed

: Substitute C2 + C2= with SNG

: Syngas from petcoke gasification produces SNG

: SNG substitutes ROG as heater fuel

Product : 1.5 mmt/yr ethylene

: Coproducts = Propylene + H2

: 730 kt/yr MEG

: 400 kt/yr LDPE

: 650 kt/yr LLDPE: 1.8 mmt/yr of ethylene derivatives

: MEG = Link in the polyester value chain


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Integration of Refinery + Petrochemicals + Gasification

Integration

Refinery Gasification

PX-4

C2complex

MEG

LDPE

LLDPE

Syngas/cogen fuel

C2+ C2=

H2

Crude Petcoke

H2

SNG

Syngas/new htr fuel Syngas/cogen fuel

PX

BenzeneReformate

Existing

New

Syngas/cogen fuel

Return

Future Chemicals

Olefins

Aromatics


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Innovate or perish

Conclusion

Competitive refining

Process lowest cost crude feed

Generate highest value petrochemical products

Integrated refinery + petrochemicals

PP from VGO via FCCs

PX + benzene from naphtha via Platformers

Ethylene from ROG Cracker

Low cost utilities

Recover C2 + C2= to feed ROG Cracker; substitute with SNG Cogen fuel from gasification for power + steam

H2 from gasification


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